Process for recovering ammonia salt from the distillation-gases of coal.



H. L. DOHERTY. PROCESS FOR REGOVERING AMMONIA SALT FROM THE DISTILLATION .GA

SES 0F GOAL.

APPLICATION FILED P111315, 1910.

Patented Nov. 5, 1912.

a sannws-snnzm Henry LDoherty,

5 vwewl'oz' v 2226 alibi/meg;

I H.L.DOHERTY. PROCESS FOR EEGOYEBING AMMONIA SALT FROM THE DISTILLATIO N GASES 0F GOAL.

APPLICATION FILED IEB. 15,-1910.

Patented Nov. 5, 1912.

3 SHEETS-SHEET 2.

5] vwg mfoz Henry LQDoherty,

44mm lemw GOAL.

H. L. DOHBRTY.

APPLICATION FILED PEB.15, 1910.

PROCESS FOR R IEGOVERING AMMONIA SALT FROM THE DISTILLATIOli GASES 0F 2 3 m in m H MW 3 m h w w @w m l Jim- L C C: C: IIIIII l v iIIfl-i filhnununu III-Ev; m w m w Q x Q mw 1 1i 2 9 3 E. 1

.HENBY, Ll nonnn'rr, or new YORK, n. Y.

rnoonss For. nneovnnrne'nnnuonmsam rnoivr THE DISTILLATION-GASES or GOAL.

eeann.

1 Application tiled February 15, 1310. Serial No. 544,095.

li o old whom it may concern:

,Be it known that I, HENRY L. a citizen of the United States, and a ct Yew city, in-the county oi; dew York and State of New York, hav invented certain new and useful Improvements in lrocesscs tor Recovering Ammonia Salt trom the :Distillation-Gases of Goal, of which the following is a specification.

- invention relates to a process for re- 7 covering. ammonia salt from the distillation,

in n of the go of coal, and, in particular, to such a s i'11 .\vl1icl1theammonia is fixed by derived from constituents of the disron gases formed contemporaneously .ithe ammonia itself. 1 l

t his application relates to-a' modification it the icess claimed in my co-pending application %,094 filed Feb; th, 1910.

,ll he cbject'ot' myinvention is to provide geese. whereby the ammonia tormed'in the destructive distillation of the coal- -may' converted intoa salt consisting, chiefly, ammonia sulfiteby means of sulfurous acid formed from the sulfur of the hydrogen iii-d. wli' formed during the distillacozu; substantially contempora y with the ammonia. ln-the usual manner of fixing the ammonia termed the distillation or gasiticat-ion' of coal, the ammonia-bearing gases are conduct d through a suitable chamber in which they are contacted wvith separately :rnanufactored sulfuric acid, fixing-the ammonia as tuninomum sulfate. This product is used as thesource of animoniator various industrial purposes but chiefly as a fertilizer-L By my-method, I am able to fiXlZhQ -ZLHHDOIHQ- iii a form that is just as available as the sulfate without thenecesslty of using any chemloal reagents otherthan' those obtained from the coal at the same timeas the ammonia.

Briefly, my invention consists -inabsorbing' the ammonia land hydrogen sulfid of the distillation gas in a partiallypurified ain=itonia liquor containinga; substantial proportion of its ammonia in the tree or hydrated condition, separately separating the hydrogen sulfid and the ammonia from said liquor, passing the hydrogen sulfid, in

" admixture-With air, through an incandescent bed'of iron oXid, mixing-the sulfurous and sulfuric acids, so formed, and the ammon a to term EmIXlZHFQOf QIIIHOHIHIH sulhte and s'ultate 'and recovering the ammonium salts.

Specification of Letters Patent.

.tom 67 of the tray 66..

Patented Nov. 55, 191.2.

In the accompanying drawings. I have shown, in diagrammatic form, an arrangement of apparatus suitable for applying my invention.

Figure l is a perspective view of the j cooling and scrubbing apparatus. Fig. 2 is a detail oi the same showing how the scrub biog liquor passes from compartment to compartment of said apparatus. Figs. 3 and 6 talten together show a diagram'ixatic elevation of the apparatus for separating the ammonia and sulfur gases from the scrub: hing liquor and making the fixed ammonia salts therefrom with the heat inter-changer shown in part section. Fig. at is a vertical diametral section through the upper heating chamber of the purifying still. 5 is a vertical diametralscction through three of the sections of the purifying still.

In the drawings. 1 the absorption apparatus. This is divided into a plurality of compartments, :1. 71. 0, (Z, c, f. g amt/2. in the design shown, each compartment having located above it a compartment (9.... 2 2 etc... respectively.) in which is cooling coil (3 3 etc.) through which the liquid, used in the compartment to wash the gas. is passed for the purpose of cooling it before introducing it into the cmnpartment in contact. with the g: The coolin is 3er-- formed in the apparatus shr vn, by the cirulation of a cooling liquid around the coils in the compartments 9.. Circulating pumps. l etc, maintain a constant circulation of liquor from the bottoms. of the compartments to the respective cooling coils. After passing through the coils i the liquid passes through some suitable *htributing device which should secure one form distribution of'the liquid across the cross-section of the compartment. In Fig. 1 is shown a part perspective of the distributing device for chamber a. This distributing device comprises a tray 66 having a perforated bottom 67. The aggregate area of the perforations should be such relatiie tothe volume of liquor circulating thatthere will always be a substantial depth of liquor on the bot- Any ordinary variation in the rate of circulation of the liquor is automatically taken care of by" "the increased rate at which the liquor passes through 6. with the increase in hood of liquor in ($6 and. vice versa. bythe dumnution-ot flow Wll'll the tall of head in {S6,

The sheet 68 forms the top of compartment (in and at the same time the bottom of the cooling compartment 2,. As shown, the liquor enters the middle portion of the coil 3 and flowing each way discharges through the connections (39 and 7 0 onto the dis tributing tray 66,, and thence passes through ture and is thus brought into intimate contact with the scrubbing liquid.

In compartment h, the gas which, here, should contain only a trace of NH and the acid gases H,,S and CO is subjected to scrubbing by a portion of previously formed ammonia liquor which has been freed, in the manner hereinafter described, from substantially all of its volatilizable compounds. The'extent to which itis necessary to remove the volatilizable gases from this portion of the liquor depends, in great measure,

upon the temperature that prevailstin it. While ammonia has a considerable aflinity for water, even weak solutions of NH in water possess an appreciable vapor tension at ordinary temperatures. It is necessary that the liquor used for scrubbing in h should have a vapor tension of its NH less than the tension of the small quantity of NH, .in the gas passing through compartment h. Usually the final traces, of NH are removed from the gas by scrubbing with fresh water. preferto use liquor that has been freed from its. volatile ammonia in order to avoidthe dilutionof the liquor that is occasioned by the use of fresh water.' The liquor inh is maintained in circulation by pump 4 as already explained. A portion of this liquor, corresponding to the volume of fresh liquor introduced through pipe 7 overflows to compartment 9 through the sealing device, shown on an enlarged scale in Fig. 2, and mixes with the liquor circulating in compartment g.

The sealing device shown is formed by two bafiles' 8 and 8,, respectively, spaced away from the wall dividing it and g. The lower part of the dividing wall is'pierced with numerous apertures 71. Under normal conditions of working the liquor level in the bottom of compartment it would be at a considerable height above the baffles 8,, and 8 say at the level R S. Since in normal working a portion of the liquor is constantly withdrawn from one ofthe compartments By my method, however, I

(cl for example) the level of liquor in this compartment tends to fall. This causes a flow of liquor from the next communicating compartment 0 through a sealing device similar'to the one described above. which, in turn, causes a flow of liquor from f to c and so on. Owing to the friction of the gas passing through the compartments and the connecting ports there is a slight graduated fall in pressure at a given level in each of the suction pipe 5 of pump 4 and is cir culated in the manner described, a volume of liquor corresponding to the overflow from handthe quantity of treated liquor introduced through 9, overflowing to comartment f. The liquor'flows in this way rom compartment to compartment, a volume being maintained in circulation in each compartment much greater than the volume of the flow from compartment to compartment. The volume of liquor supplied through the pipes 7 and 9 depends, in great measure, upon its content of free ammonia. It is necessary to introduce in the liquor the quantity of free ammonia that will suffice, in connection with the ammonia already present in the gas, to form sulfid and carbonate', respectively, with the H 3 and CO. of the foul gas. When t-heprope'r quantity of 'free ammonia is supplied in the liquor,

substantially all of the 11 s, co, and NH,

is removed from the foul gas. In my preferred method of working, I withdraw the liquor bearing the H S, CO a'ndNH from compartment cl through pipe 10 and run it tothe ammonia sulfid recovery plant. This is shown diagrammatically in Figs. 3 and6.

11 is the still in which the impurities removed from the gas are separated from the liquor, and about half of the ammonia in the latter again converted to the free or hydrated condition. 11 has, in its lower portion, three chambers or retorts, 12, 13

and 14, Upon the uppermost of these cham-.

hers 12, is built up the'st-ill proper. This is composed of a plurality of sections, '15}, 15 15 etc., arranged as shown in Fig. 5.

16 is a heater-cooler, consisting of a cylindrical tank having an upper and lower tube-sheet (l7-and :18, respectively) with tubes 72 supported thereby. The chamber included between the tube sheets isdivided by partition 19 into two Compartments, 16 and 16". The liquor passing: throughmpipe c absorbed from"t'hegas, enters below the 5 tube-sheet '18, and'passes up through the tube's'FQ to the spaceaho e the uppertube sheet 1'1 During its ,7 upward passage through tlie" tubes, the "liquor is heatedlby two streams of hot liquor passing in the contrary direction through the compartments IGf-and' 16 1' Now' the ammonium sulfid and ammonium carbonatebegin to disso- Gist-em aboutTSS fand124 Fair, respectively} Therefore in'p afs'sing through 16 the ammonium salts of the foul liquor are par tiallyldissociated with the evolution of aiicl*(lfl() =i These reactions are endothermic in character andthere is, therefore, a con siderable quantity of heat rendered latent dill-ring; the passage of the foul liquor through the heater-cooler. @This heat ab:

'stir-ption fincreasesthe thermal capacity of tli' foul 'liquorand thus increases the etfi uency-"or heat recuperation from the hotpurified liquorL' The "gases evolved from liquor in thecourse of this heating'clis-a' tha -g8 from lfithro'ugh tl e'pipe 20into one toft as slum 10 0f stillyll he sections .(15 Fleet-heated liqiior'fion 16 enters onezof the sections 1 (1553s; shown){ The section fwl iiclij the foul liquor is introduced should vselected so that the gases passing through that section have a temperature but. little abo e tha-t of the foul liquor itself.- {From I 15 (or any others-ection atxyhich it is en;- tered) the liquor flows from section to. secti on. througlrthe',sealed oyerfiorv passages 21 into-theupper heating-"chamber 12. As i the liquorpasses through thesections 15, 4 itl s subjecteil'totheactiorrof the'hot gases .ydischarging n-mn the compartment 12,

which pass-through thegaspassages 46 11.11

' der the hood if'qand theirpass cthroughthe perforations QSinthe submerged portion of the hood; In, bubbling through the sealing liquor-in the diiterent sections, the hot gases v gineuppart of't'heir heat to the fo-ul'liquor, still further increasing'its temperature,and, dissociating still; more of its ammonium salts; ;'-1Zhe; liberated lil,S a11 cl CO sepa-j from therliquor andjoinsthe, gaseous our ent passing through-the,still; Thezdisr, sociation. of the aiinnoniumsalts is material..,ai;d{ the: eooling ot the foulf gases.

. The ammonialiberated in the dissociation of the" salts iir-igreat part, retained in the liquo" since its coefiicient of. absorption is; many itjin es that; ot H; and G0,, at; the tentperature pre\ 'ai l ing I 111; In thegheats. ing chamber l2, the li-quoi; i heated to 1 a sereral degreesbelow its boil== in point under; the pressureprevailing inn starch; 1 nth-eat :the iliqnergin :12 v

, is "drawnoff from 12 through pipe forced bypumpfle to the top of compart- "ment 16" of heater-cooler 16. The other vailing, the capacity of the still with refergenceto the gas wash'enetc; Usually, I aim to maintain in 12 a temperature of from 6 tfo l2 degreesbelow the boiling. point of the liquor under the pressure obtaining in 12. 'Ijhis pressure dependsof co'urse, upon the altitude of-the locality. in which the treatnient is carried out andupon the backpressure caused by the seals in thesections of the still. Ifthe barometric"pressure in .12- is about 25.9 .inches of mercury, I would, preferably, maintain the temperature in 12 at about 1979 to L8 Fair, nearly as may be, While at a barometric 'u essure of say 31.3 inches in 12 1 would, preferably, heat the liquor -therein at a temoerature of about 2043 to 206 Fahm At this temperature the ammonium salts are very rapidly dissociated, the H 8 and CO liberated being inimecliately, evolved While the liberated ain inonia is fortlie great part retained in the liquor owing tothe relatively great ceetlicient of absorption .of'irater for. as compared with those for 1' Sand CO What ammonia is driven not? from the liquor (in 12.7is reabsorbed in the current of foul liquor entering the still and in the special Wash. liquor-introducedinto the 'upper section ofxthe still as'here ai'te fdescribed, andis thus constantly returned in ,tlieliquor current entering 12. In my pre ferred method of Working, the liquor discharging from 12, Will have hadfrom 50 to SO'per cent. of itsH Sand CO, elimillfllGClWltll a reduction in its percentage of ammonia ofonlyabout This liquor will therefore have from 50 to per 'cent. of its. ammonia in the free or' hydrated condition'. The. liquor discharging from 12 is dividedinto two sections; ,The main 'streaiq -flI1( stream is permitted to pass through the OVQlflOWlQ' into the boiling;compartment 13.? The'proportion of free ammonia inthe liquor discharging from 12 may he"in-- creasech'bu'tat the expense of the product1on.o;t..-a Weaker liquor. foundith'at the method of gives the most economical IQSUltS.

ammonia Therefore I have- .YO'llililg outlined i lrn conipartment '13, the portion of thei liquor which passes th'reinto is subjected to active'boiling until the NH,;',-CO and H S :have been completely driven The gases evolved inv13 together with those evolved in reto'rt-let as described below, ar'e'divided into 1 two streamsx The larger-stream 1S drawn j o'fifv from 13 through atlie pipe 32 as described below The excessg if any, (my this first .rpiortion i passesthroiiglr- 46. in the bottom)? inder epresses the level-of liquitl 'iuicer, 4 71 "til the perforation 8 iii ti of 47''" are ans sle these perforations and bubbles up through 'the liquor in 12. As the temperature of the thehood47, depress the level of the liquid 4 into two streams, one being drawn off through B9I1diPg the ammonia incrementpf the soda industry. It consists of a. number;

under-."the: hooduntil the perforations 48 :in its flange portion are unsealed, through the perforations and bubble, up through the liquor in 15,,thence through" the {sections above in the same-.manner. The .boiled liquor discharging from 1 3 is subdivided pipe 25 and raised by pump 26 to the top of compartment 16. The other subdivision of the liquorpasses through the overflow 27 intothe liming compartment 14. The liquor leaving 13 contains only the fixed salts of ammonia-sulfate, chlorid, etc: The proper quantity of milk of lime is run into 14, through the pipe '28 to combine with the acid of the fixed ammonium salts and-liberate the N H This latter passes up through the. pipe 29 into the vapor space of 13, and joins the gaseous current discharging: from 13. The liquor discharging from 14,'whichl1as been freed from all its ammonia, both volatile and fixed, is permitted to run to waste.

The cooled liquor discharging from compartment 16'- is divided into two streams. One of these streams passes directly to the circulating pump of compartment h, through the pipe 7, while the smaller stream is conducted to the uppermost section 15 of the still" 11 through the pipe 31. Overflowing from 15 through-the sealed overflow passage it passes into the section 15", and thence downward through the different sections to section 15", where it mi'ngles with thefoul liquor entering that section. The gases passing up through the still are subjected to scrubbing by the descending liquor, all,of their contained NI-I being absorbed, while the bulk of the H 8 and CO passes throughunabsorbe d, and discharges from the still through the pipe 34. g

The gases from 13 and 14 are relatively strong in ammonia. The gas from 14 is composed almost entirely of ammonia and steam, while the ammonia constitutes nearly one-half of the fixed gases evolved-in 13. The gases from these two compartments, after condensation, are therefore very strong in ammonia. Therefore, I prefer to remove from the system, at this point, its increment in ammonia. I withdraw from 13 through the pipe 32 the proportion .of its vapors which'carry a quantity of ammonia corresystem, and lead them to the purifiers 36 and 37, which are charged, respectively, with iron oxid and lime. The pipe 32 should be cooled to cool the gases and condense the water vapor present, the condensed liquid being returned to the compartment 13 through the pipe 32, by gravity; or a cooling coil (not shown) may be introduced on 32 between 13 and 36. The gases from 32 pass through the purifiers 36 and 37 and the hydrogen sulfid and carbon dioxid are here separated from the ammonia. The pure ammonia passes through the pipe 38 tojoin the treated eflluent gases from 11 in the condensing chamber 45. The efiluent gases from the still 11, pass through the pipe 34 to fan 39. From 39 the gases pass to the oxidizing chamber 40, in which is a bed of iron oxid (or other suitable material) 41, supported by bars 42. This must initially be heated to nearly low' redness but,

after the reaction has been started, the heat developed is suificient to maintain the tem- I perature of the oxid. Through the damper 43, air is drawn into the gases by the suction of fan 39 and the mixedstill gases (CO H S, N, etc.), together with the air, passed through the bed of oxid in 40. The CO is unchanged, but the H 5 is decomposed by the'iron oxid in the presence of air with the formation of H 0 and S0,, chiefly, and some 80,. The efiiuent gases from 40 pass through the conduit 44 to the condensing chambers 45. Here they mix with the ammonia entered through the pipe 38. The S0, and S0 having a reater affinity for the ammonia than the 3 0 the ammonia combines with the sulfur acids and water to.

When, however,

low (below Fah.) there is formed more or. less of a carbonated salt of ammonia, of a composition corresponding to the commercial salt known as sesquicarbonate of ammonia. This condition seldom occurs in the case of distillation gases from coal but will sometimes be met within the case of pro ducer gas. When the deficiency of sulfur compounds is considerable -I find it advisable to introduce an anxiliary condenser, 49, into which the gases from 45 are forced by blower .50. This auxiliary condenser may be of any suitable type and, as shown,- is a,

common form of absorption tower usedi'n of superimposed sections, 51, 52,53, etc, the section 51- be'mgs1mplyan open cylindr cal "chamber-$- l he 'othersections are alike in construct-ion,each has an opening, 56, in its saturation point a carbonatedsalt of ammonia crystallizesont The crystals work down with the liquor through the openings 56fa1idare Withdrawn fronri!) with the li-cp uor through-the pipe 61." The liquor discharges on a screen, 62, in the'u-pper partof i Wit-ln tankl 63,0n which the crystals are interceptedaand'may'beremoved at intervals. The strainediiiother'liquor is drawn ofl'tt rom the bottom of-63yijy circulating pump (El, and forced'throug h the cooling coil 65 and pipe 60 "to-the top of 4 9 to be again passed through. "Usual ly the Water vapor that carried into -the condenser 45 by the' gases from 40 will suffice to form the crystalline salts of aminon'ial W'Vhen there is a deficiency of sulfur compounds, however, the salt :crystallizingin 49 Will fix some of the Water 'ofthe-mother liquor; It is generally necessary,therefore, to add Water to the liquor from time to tiine.

' iThemethod 'of'scrubbing the crude gas, whichis-herein described, is not claimed in this applicat-ion, specifically, as it-is claimed in anothercopending application, filed here-' The process. of converting easily decomposable ammonium compounds comprisnsz described my invention, What (I ing sulfur compoundsof ammonia into ino rest'able salts which comprises decompos ing the said ammonium compounds by means of: heat" to form'f-free ammonia andgases comprisinghydrogen siilfid, separating am -n'ionia from the ga'ses containing hydrogen sulfid, mixing oxygen-containing gas with th'e said hydr en-sulfid-containing gases,- pas'sin'g lthe resulting niix'ture in contact' With'a catalyticmater'ial maintained at the proper temperature for reaction and mixing the irev'iously eparated a m'n' 011121, with the gases il'sllltlll from the contact of "the said gas -inixture with sa d catalytic ii atei'ial.

2L -Tlie 'pi ocess,of converting mixed am Jvi' ,-i-. ,6 mom-um sulf i'dsvand: carbonates into more alts; which comprises decomposing d compounds by"means of heat to reef ai fnonia and hydrogen-sulfid 'es, separating liberated amtrioxid, mixing with monia from the Hydrogen-solfid-contair' gases of the'said compounds, oxidiiin furcompounds of the said hydroge containing gases antlinigiing the previous y separated ammonia with the oxidizedsultfin compounds, whereby mixture of ammov niun'i salts of sulfur-oxygen acids 'isyformed.

3. The process of converting mixed gimmouium sulfids and ear-homes, into more stable" salts which comprises dec (imposing the said compounds by means of hciit'to liberate ammonia and acid gas, separating the liberated aminoi'iiafrom theacid gases of the said compoi-inds', oxidizin'gthe hydro genv sulfid otthe said acid gases in most part to'sulfur dioxid and adding the previously separated ammonia to the sulfur dioxid and. free carbon dioxid, whereby'amixed salt of oxidized sulfur compounds of ammonia is formed. f k

'4. The process of converting ammonium sulfide into oxidized sulfur salts of ammonium which comprises, decomposing the said ammonium sulfids by. heatingthe same to "liberate ammonia and hydrogen sulfid,

separating the liberated ammonia from the liberated hydrogen sulfid; oxidizing the said h xlrogeu sullid to sulfur dioxid and sulfur the ox dized sultur gases the previously separated ammonia and coolingthe' mixturedown to the point of solidification of ammonium sultite, w iereby a'mixture otammouium sul'lite and sulfate is formed. i

5'. The process otconverting mixed ammonium sulfids and carbonates into more. stable salts. which comprises decomposing the said compounds by means of heat to liberate ammonia, hydrogen sulfid and carhon dioxid, separating the liberatedhmmonia from hydrogen sulfid and carbon diQ oxid of thesaid compounds, oxidizing said hydrogen sulfid to' sulfur-oxygen compounds and Water, mixing the resulting gases with said separated ammonia, and cooling the re sulting mixture below the point of solidification of the resulting ammonia salts, whereby a mixture of ammonium salts of sulfur-oxygen acids is obtained.

6. The process ofmaking ammonium salts from gas containing ammonia and hydrogen sultid which com irises separating the ammonia and hydrogen sultid tr'omsaid gas, separating the hydrogen sulfitl from said an'imonia,' adding suflici'ent oxygen to said hydrogen s'ultid to convert the same sulfur dioxi'd and Water, passing the said mixture of hydrogen sulfid and oxygen through abedi'ott' metallic oxid maintained at a reactive temperature, whereby the said hydrogensulfiif '1 converted to sulfur dioxid and Water,'mixing the separated ammonia with the sit-formed sulfur dioxidand Water and condensing the ammonium sulfite' formed l 1 into 7. The process of making ammonium salts I from gas containing ammonia and hydrogen sulfid which comprises separating the ammonia and. hydrogen sulfid from said gas, separating the hydrogen sulfid .from said ammonia, adding sufiicient air to said hydrogen sulfidto oxidize the same to sulfur dioxid and water, passing the mixture of air andhydrogen sulfid in contact with a catalytic material capable of causing the oxygen of the gaseous mixture to combine with the hydrogen sulfid of the same, whereby a sulfur-'dioxid-bearing gasis obtained,

mixing the separated ammonia with said sulfur-dioxid-bearing gas and condensing the ammonium sulfite formed.

8; The process of making ammonium salts from crude coal gas which comprises contacting said gas with aliquor-containing withdrawing said liquid from contact withv said hydrogen" sulfid, subjecting said liquid free ammonia, whereby the ammonia and sulfurcontained in said gas are absorbed by said liquor, withdrawing said liquor .from contact with said gas, subjecting said liquor to heating, whereby ammonia and hydrogen sulfid are evolved from said liquor, absorbing the evolved ammonia in a liquid,

to heating to liberate said ammonia, oxidizing'aaid hydrogen sulfid to form oxids of sulfur and water, and mixing the said liberated ammonia with said oxids of sulfurto form fixed ammonium salts.

9. The process of making ammonium salts from crude coal gas which comprises contacting said gas witha liquor containing 'free ammonia, whereby the ammonia and acid'components of the said gas are absorbed I by said liquor, to form foul liquor, .With

drawing said foul liquor from contact with .said gas, subjecting said foul liquor to heatmg, whereby a portion of the ammonium salts in said liquor are dissociated with the elimination from said liquor of a major proportion ,of its acid constituents and a minor proportion of its ammonia, to form purified liquor, cooling the major portion of said ffiurified liquor and using it to scrub the ammonia and acid components from a fresh portion of crude coal gas, subjecting the minor portion of said purified liquor to boiling tov distil ofi substantially all of its volatilizable gases, subdividing the boiled minor -portion of said purified liquor into two streams, cooling both of said streams, contactingthe cooled liquor of one of these streams with another portion of crude coal .gas after the latter has been scrubbed by said purified liquor, contacting the cooled liquor of the second of said streams with the .gases eliminated from said foul liquor,

- whereby the minor portion of the ammonia eliminated from the said foul liquor is 'removed from said gases, withdrawing said second stream from contact with the residualgases, subjecting said second stream to boiling to free its absorbed ammonia, mixing oxygen with said residual gases, contacting such mixture with a catalytic material to oxidize the sulfur compo-unds in; the mixture, adding to the so-fo-rmed gaseous mixture the ammonia freed from said, second stream of liquor, and subjecting the mixed gases resulting fromsuch addition of ammoima to cooling, whereby fixed ammonigsalts.

salts of said liquor are dissociated with the.

elimination from said liquor of themajor portion of its acid components and a minor portion of its ammonia, to form a purified liquor, cooling the major portion of said purified liquor by said foul liquor, and using it to scrub the ammonia, hydrogen sulfid and other impurities from a fresh p'or-. tion of crude coal gas, subjecting the minor portion of said purified liquor to' boiling to distil off substantially all of its volatilizable gases, contacting such distilled gases with another portion of purified liquor, and adding the unabsorbed portion of such distilled gases to the gases eliminated from another portion of said foul liquor, subjecting a fraction of the boiled minor portion of said purified liquor to further boilingvwith lime to expel its fixed ammonia, adding the ammonia so expelled to the ammonia distilled from the minor portion of said purified liquor, subdividing the residual portion of the boiled minor portion or said purified liquor into two streams, cooling both'of said streams, contacting the cooled liquor of one of these streams with another portion of crude coal gas after-the latter has been scrubbed by said purified liquor and then adding the stream to the purified'liquor to be used to scrub a fresh portion of crude gas, contacting the cooled liquor of the second of said streams with the gases eliminated from another portion of foul liquor, whereby the minor. proportion of its ammonia eliminated from said'foul liquor is removed from said gases, withdrawing said second stream from contact with the residual gases, subjecting said second stream to boiling to free its absorbed ammonia, and purifying said ammonia, mixing a suificient proportion of .air said residual gases t9.

oxidize somewhat more of the hydrogen sulfi d of said residual gases than the proport1on-equiva1entto the ammonia freed from said second stream, contacting said mixture of residual gases and air with oxid of iron maintained at an mcipientred heat, whereby a somewhat greater proportion of sulfur oxids are formed than that equivalent to the.

ammonia freed from saidsecond stream,

mixing the gaseous mixture obtained by contactingthe residual gases andair with the and sulfate so formed.

Signed at New York city in the county of day of February A. D. 1910.

HENRY L. Witnesses:

L. G. COLEMAN,

THOS. I. CARTER.

DOHERTY.

New York and State of New York this 12th 

